Plastics material substrate having a silicon coating

ABSTRACT

Plastic material-comprising surfaces of a substrate are coated with elemental silicon by cold gas spraying by injecting a powder containing silicon into a gas and powder with a high velocity onto the substrate surface, such that the silicon forms a firmly adherent coat on the substrate surface comprising the plastics material. Apparatuses having such silicon-coated surfaces are useful in minimizing contamination of polycrystalline silicon production, processing, packaging, and transport.

CROSS REFERENCE TO RELATED APPLICATIONS

This application is the U.S. National Phase of PCT Appln. No.PCT/EP2015/069494 filed Aug. 26, 2015, which claims priority to GermanApplication No. 10 2014 217 179.2 filed Aug. 28, 2014, the disclosuresof which are incorporated in their entirety by reference herein.

BACKGROUND OF THE INVENTION

1. Field of the Invention

The invention relates to silicon-coated plastics material substrates.Silicon-coated plastics material substrates may be used to makelow-contamination or contamination-free surfaces of product-contactingcomponent parts of plants or apparatuses for production, furtherprocessing, and logistics (packaging/transport) of polycrystallinesilicon.

2. Description of the Related Art

Polycrystalline silicon (polysilicon) is, for example, deposited frommonosilane or from chlorosilanes such as trichlorosilane onto thin rodsby the Siemens process to obtain polycrystalline silicon rods which aresubsequently comminuted into polycrystalline silicon chunks (polysiliconchunk). Once comminution into chunks has been carried out, the chunksare typically graded into particular size classes. Once sorted andgraded, the chunks are metered out to a particular weight and packed ina plastics material bag. The chunks are optionally subjected towet-chemical cleaning prior to packing. The chunks typically need to betransported from one plant to another between the individual processingsteps, e.g. from the comminution plant to the packing machine. Thistypically involves intermediately storing the chunks in buffercontainers which are typically plastics material boxes.

Polysilicon chunk exhibiting a very low degree of contamination isdesired for applications in the semiconductor and solar industries. Itis thus necessary for the comminution into chunks, the sorting andgrading, the metering-out and the packing to be performed in a verylow-contamination fashion.

One process for sorting, grading, metering-out and packing of chunks isdisclosed in US 2013309524 A1. The polycrystalline silicon is intiallyportioned and weighed before packing. The polysilicon chunks aretransported via a conveyor channel and separated into coarse and finechunks using at least one sieve. The chunks are weighed using a meteringbalance and metered out up to a target weight before subsequentlyconducted away via a removal channel and transported to a packing unit.The at least one sieve and the metering balance preferably havesurfaces, at least in part, of a low-contamination material, for examplea hard metal. The sieve and metering balance may have a partial orcomplete coating. The coating employed is preferably a material selectedfrom the group consisting of titanium nitride, titanium carbide,aluminum titanium nitride and DLC (diamond-like carbon).

EP 1 334 907 B1 discloses an apparatus for cost-effective fullyautomatic transporting, weighing, portioning, filling and packing of ahigh-purity polysilicon chunk, comprising a conveyor channel for thepolysilicon chunk, a weighing apparatus connected to a hopper,deflection plates made of silicon, a filling apparatus which forms aplastic bag from a high-purity plastic film and comprises a deionizerwhich prevents electrostatic charging and thus contamination of theplastic film with particles, a welding device for the plastic bag filledwith polysilicon chunk, a flow box which is mounted above the conveyorchannel, weighing device, filling device and welding device and preventscontamination of the polysilicon chunk by particles, and a conveyor belthaving a magneto inductive detector for the welded plastics material bagfilled with polysilicon chunk, all component parts coming into contactwith the polysilicon chunk being sheathed with silicon or covered with ahighly wear-resistant plastic material.

US 20120156413 A1 describes a two-layer construction of plasticsmaterial sheets on a metallic base body. The base body is faced with thesheets, the sheets being secured using bolts or the like made ofmaterial the same as or similar to the material from which the sheetsare made. Transport channels and containers/hoppers coming into contactwith polysilicon may be similarly formed.

U.S. Pat. No. 6,375,011 B1 proposed a process for conveying siliconchunk comprising passing the silicon chunks over a vibratory conveyorconveying surface manufactured from highest-purity silicon. However, ithas become apparent that loosening and even rupture of the conveyingsurface silicon facing can occur during operation of such vibratoryconveying units. There is thus also a risk of product contaminationduring conveying.

Granular polycrystalline silicon or “granular polysilicon” for short, isan alternative to polysilicon produced in the Siemens process. While theSiemens process affords the polysilicon as a cylindrical silicon rodthat requires time- and cost-intensive comminution and possibly evencleaning prior to further processing thereof, granular polysiliconexhibits the properties of a dry bulk material and may be employeddirectly as raw material, for example for single-crystal production forthe photovoltaic and electronic industries.

Granular polysilicon is produced in a fluidized bed reactor. This isaccomplished by fluidizing silicon particles using a gas stream in afluidized bed and heating the bed up to high temperatures using aheating apparatus. Addition of a silicon-containing reaction gas such asmonosilane or a chlorosilane, optionally in a mixture with hydrogen,brings about a pyrolysis reaction at the hot particle surface. Thisdeposits elemental silicon on the silicon particles and the individualsilicon particles increase in diameter. Regularly withdrawing particlesthat have grown in diameter and adding of relatively small siliconparticles as seed particles allows the process to be operated incontinuous fashion with all the attendant advantages thereof.

U.S. 20120183686 A1 describes metal tubes whose interior surfaces haveat least a partial coating of silicon or a material comprising silicon.Particulate silicon is transported through these tubes. The materialcomprising silicon may be, inter alia, fused silica, silcon carbide orsilicon nitride. Such tubes may be used in particular in the productionof granular polysilicon, wherein seed particles or granular polysiliconare transported through such a tube.

U.S. Pat. No. 6,007,869 A discloses a process for producing granularsilicon. The inside of the reactor tube made of metal, for example ofstainless steel, has a facing of high-purity silica and the outside ofsaid tube has a casing of insulation material having a low thermalconductivity, for example silica material.

The production of high-purity granular polycrystalline silicon requiressilicon seed particles. Gas jet mills are known for the production ofsuch silicon seed particles, for example from U.S. Pat. No. 7,490,785B2. In one embodiment the parts of the apparatus coming into contactwith the silicon particles consist of an outer metallic shell having aninterior wall provided with a coating. Silicon in mono- orpolycrystalline form or a plastics material are employed as the coating.

The abovedescribed jet mills are not suitable for producing silicon seedparticles having particle sizes greater than 1250 μm. However, recoursemay be made to roll crushers to produce silicon seed particles of such asize. JP 57-067019 A discloses the production of silicon seed particlesby comminution of polycrystalline silicon in a roll crusher andsubsequent fractionation by sieving. The rolls are manufactured fromhigh-purity silicon.

U.S. Pat. No. 7,549,600 B2 discloses a process for producing siliconfines by comminution in a crushing plant and grading of the fines, aportion of the crushed material having an edge length less than or equalto the maximum edge length of the desired silicon fines (fraction 1)being collected in a collection container 1 and the portion of thecrushed material having an edge length greater than the edge length ofthe desired silicon fines (fraction 2) likewise being collected. In oneembodiment a portion of the fines having an edge length less than theminimum length of the desired silicon fines is separated out of fraction1 and collected (fraction 3). The obtained fractions 1 and 3 may be usedas seed particles for deposition of polycrystalline silicon in afluidized bed process. The crushing tools have a surface made of a hardmetal (particular preference being given to tungsten carbide in a cobaltmatrix) or of silicon.

It is known from the prior art to face plant parts with silicon orplastics material or to manufacture said parts entirely from one ofthese materials. Hard metals are also used as low-contaminationmaterials of construction when handling silicon. Facings are preferablesince a metal base body confers greater stability on the plant part.However, the facings with plastics material or silicon known from theprior art are not always stable. Abrasion and consequent damage to thefacings may occur. This can result in the plastics materials of thefacing contaminating the polysilicon, particularly with carbon. Damageto the facing furthermore exposes the surface of the generally metallicbase body which can result in contamination of the polysilicon withmetallic particles. It may be possible to further reduce the surfacecontamination of polysilicon chunks by wet-chemical cleaning though thisentails additional costs and complexity.

SUMMARY OF THE INVENTION

The object to be achieved by the invention arose from the problemsdescribed above relative to preventing contamination of polysilicon.This and other objects are achieved by a process for silicon-coating aplastics material-comprising surface of a substrate by cold gasspraying, comprising injecting a powder comprising silicon into a gasand applying said powder with a high velocity to the substrate surfacecomprising the plastics material, so that the silicon forms a coatfirmly adherent on the substrate surface comprising the plasticsmaterial. The object is also achieved by an apparatus which at least inpart comprises a surface made of a plastics material, wherein theplastics material surface has a firmly adherent silicon coat.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 shows an SEM image of a substrate made of polyamide that has beenprovided with a silicon coat.

FIG. 2 shows an SEM image of a cross section of the substrate.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS

Preferred embodiments of the process and of the apparatus are apparentfrom the description which follows and the dependent claims.

Cold gas spraying (also known as kinetic spraying) comprises applyingpowder to a support material (substrate) at a very high velocity. Thematerial (powder) to be sprayed is typically introduced to the gas via apowder conveyor, heated up to several hundred degrees and introduced tothe spraying system comprising a de Laval nozzle which accelerates thegas comprising the introduced particles to supersonic velocities.

From a process engineering standpoint, cold gas spraying distinguishesitself from thermal spraying by comparatively simple process controlsince the only process parameters that may be directly contolled are gaspressure and gas temperature.

The gas jet accelerates the injected particles to such a high velocitythat, in contrast to other thermal spraying processes, even withoutpreceding incipient or complete melting, the particles form a coat onimpacting the substrate that is homogeneously closed and firmly adherenton the substrate surface. The kinetic energy at the time of impact isnot sufficient to result in complete melting of the particles.

In the context of the present invention, description of the silicon coatas firmly adherent is to be understood as meaning that low levelmechanical action, for example rolling or sliding of silicon materialover the coat, results merely in wear due to attrition and not in anyparticles breaking out of the coat.

The process may be used to silicon-coat a very wide variety ofsubstrates made of thermoplastic, thermosetting and elastomeric plasticsmaterials.

Coating metallic substrates employs gas jet temperatures of up to 950°C. The gas pressure may be up to 50 bar.

Coating plastics material-containing surfaces requires markedly lowergas pressures and gas temperatures. The gas temperature is preferably inthe range of from 200° C. to 550° C., it being necessary to take intoaccount that erosion (material removal at the substrate) occurs on anyplastics material type above a certain temperature.

The gas velocity is preferably several times the speed of sound a (e.g.971 m/s for helium or 334 m/s for nitrogen at 0° C.); the gas jetaccelerates the particles to velocities of from 500 m/s to 1500 m/sbefore impact on the substrate surface to be coated.

By contrast to hard, ductile and relatively highly thermally resilientmetallic surfaces, plastics material substrates have elastic, plastic tobrittle properties and relatively low thermal resilience. To apply adurable silicon coat on a plastics material surface, the parameters ofspray distance to the substrate surface, amount of powder introduced,feed rate of the robot and associated optimal particle size are tailoredto one another. The quality of the sprayed-on silicon coat isadditionally determined by process parameters dependent on the geometryof the body to be coated. For example, for flat substrates theparameters line spacing and line overlap are crucial for a meanderingtraverse path of the spray jet on the substrate surface. By contrast forrotationally symmetrical bodies the rotation of the substrate body,clamped on a lathe for example, plays an essential role.

The silicon particles ideally possess exactly the amount of kineticenergy required to plastically deform the plastics material. Theparticle thus penetrates by mechanical deformation into the plasticsmaterial surface (just far enough) for said particle to exhibitmechanical adhesion and also to become part of the silicon coating.

Process gases employed in the cold gas spraying are preferably the inertgases nitrogen, helium and mixtures thereof, it being particularlypreferable for these gases to be employed in high-purity form.High-purity is to be understood as meaning that impurities are presentin amounts of less than 5 ppmv.

The use of high-purity gases avoids incorporation of contaminants, forexample metals, dopants or carbon, into the silicon coat by means of thegas.

The de Laval nozzle is preferably made of silicon carbide or of tungstencarbide in a cobalt matrix.

The powder preferably comprises polycrystalline silicon having grainsizes of from 1 to 400 μm, more preferably having grain sizes of from 20to 80 μm. Grain sizes of from 20 to 80 μm produce a particularlyhomogeneous coating.

One preferred embodiment employs silicon dust particles formed as aby-product in the milling of granular polycrystalline silicon to affordseed particles. A detailed description of a suitable milling process maybe found in U.S. Pat. No. 7,490,785 B2. The air jet mill preferably hasa facing of a high-purity material of construction, particularpreference being given to silicon. This minimizes contamination both ofthe seed particles and of the silicon dust generated.

Silicon dust particles from the milling exhibit a low level ofcontamination with metals that sums to no more than 80 ppbw.

The maximum levels of contamination with metals are preferably:

Fe: max. 10 ppbw;

Cr: max. 5 ppbw;

Ni: max. 5 ppbw;

Cu: max. 5 ppbw;

Zn: max. 12 ppbw;

Na: max. 5 ppbw.

The maximum levels of contamination with boron and phosphorous arepreferably 25 ppta and 200 ppta respectively.

The maximum level of carbon contamination of the particles is preferably10 ppmw.

The process preferably produces a coat thickness of between 1 and 500μm. A coat thickness of between 5 and 20 μm is particularly preferredsince this thickness results in particularly good adhesion and durabiltyof the coating.

The plastics material substrate is preferably made of polyethylene,polypropylene, polyamide, polyurethane, polyvinylidene fluoride,polytetrafluoroethylene or ethylene tetrafluoroethylene (ETFE). Saidsubstrate preferably has a thickness of at least 1 mm.

It is apparent that a tight-closed and homogeneous silicon coat having acoat thickness of about 15 to 20 μm has been produced on the polyamidesubstrate.

The plastics material employed preferably has a hardness of at least 40Shore D. The use of LDPE (low-density polyethylene) is particularlypreferred.

Also particularly preferred is the use of polyurethane having a hardnessof 55-95 Shore A. It is possible to produce particularly homogeneoussilicon coatings on such a substrate.

Shore hardness is defined in the standards DIN ISO 7619 parts 1 and 2and DIN 7868-1.

Application of a polycrystalline silicon coating hardens the plasticsmaterial substrate. This is associated with reduced wear of the plasticsmaterial surfaces.

Silicon coatings also minimize contamination with carbon from theplastics material substrate.

One embodiment provides a metallic base body having a plastics materialcoat or facing disposed upon it, the plastics material coat or facinghaving a silicon coating. The surface of the metallic base body may havea plastics material coating or facing on part or all of its surface.

It is preferable when at least the part of the base body that may comeinto contact with the product to be processed or transported has aplastics material coating or facing and a subsequent silicon coating.The silicon coat serves as the product-contacting coat. The plasticsmaterial facing preferably serves as a detection coat for detectingdamage to the silicon coating. To this end, the detection coat comprisesa substance detectable on the product. Damage to the facing isdetectable via contamination of the product with the detectablesubstance. The product is preferably polycrystalline silicon. Examplesof substances readily detectable on polycrystalline silicon includecarbon and metals. Consequently, detection coats which are made ofplastics material and comprise carbon or metals are particularlypreferred.

In one embodiment the seed crystal feeds and product withdrawal sectorsin a fluidized bed reactor for producing granular polycrystallinesilicon comprise silicon-coated plastics material surfaces.The operatingtemperature in these regions is typically less than 250° C.

The usage of the silicon-coated plastics material substrates accordingto the invention is generally restricted to “cold” processes, namely toa temperature range of up to 250° C. However, this applies to virtuallyall areas of the polysilicon production chain except the actualdeposition and the immediately adjacent components subject to greaterthermal stress.

It is advantageous that substrates which have complex geometries—andcannot be protected with facings—may also be easily coated. Intercoats,for example adhesion promoters, are not necessary, i.e. the silicon maybe directly sprayed onto the plastics material.

The process is moreover highly economic since processing results inbarely any silicon losses and only low process temperatures arenecessary. The process is altogether more cost-effective andtime-efficient than conventional processes for facing plant parts.

Defective coating sections may be repaired relatively easily andcost-effectively. Damaged sections are eliminated by local respraying ofsilicon onto the sections. By contrast, defective facings requireremanufacturing of the facing components from scratch.

Even when the coat comprising silicon is damaged, a high product qualityis still assured due to the adjacent plastics material substrate.

Transportation means benefit from reduced weight since facings are notrequired.

The features cited in connection with the abovedescribed embodiments ofthe process according to the invention may be applied correspondingly tothe apparatus according to the invention. Conversely, the features citedin connection with the abovedescribed embodiments of the apparatusaccording to the invention can be applied correspondingly to the processaccording to the invention.

The features cited in connection with the abovedescribed embodiments ofthe process according to the invention may be implemented eitherseparately or in combination as embodiments of the invention. Saidfeatures may further describe advantageous embodiments eligible forprotection in their own right.

One embodiment comprises silicon-coating the interior of anon-pressurized single-walled storage and buffer container for granularsilicon, where the container is made of plastics material.

A further embodiment comprises providing a pressure-rated storage andprocess container, comprising a metallic pressure-rated wall and aplastics material inner coating, for example made of fluoroplasticsmaterial, with a final surface coating of silicon.

Also comprehended is silicon-coating the interior product-contactingsurfaces of transport and storage containers or transport boxes forpolysilicon chunk, where the containers or boxes are made of plasticsmaterial, for example of polyethylene.

Compared to containers having a facing made of silicon or glass, thesecontainers have a lower weight, a greater useable volume and are alsosimpler to manufacture.

A further embodiment comprises silicon-coating the interior surfaces ofnonmetallic pipes, for example pipes made of polyvinylidene fluoride(PVDF).

A further embodiment comprises providing a pressure-safe metallic pipe,the interior of which is faced with plastics material, preferably withpolytetrafluoroethylene (PTFE), with an additional silicon coating onthe plastics material.

A further preferred embodiment comprises providing a pressure-safemetallic pipe, the interior of which is coated with plastics material,preferably with ethylene chlorotrifluoroethylene (ECTFE), with anadditional silicon coating on the plastics material.

It is likewise possible to provide a silicon coating to plasticsmaterial surfaces subject to stress due to sliding but to littleabrasive stress due to the product. This reduces wear and thus alsoreduces product contamination by the plastics material (primarily bycarbon).

It is likewise possible to silicon-coat anti-splash facings made ofplastics material, for example on filling pipes, suction hoods, andcrushing tables.

One embodiment comprises silicon-coating sieve frames and covers ofsieving machines for grading granular silicon and chunks, where theframes and covers are made of plastics material. It is preferable toemploy sieve screens made of particularly wear-resistant plasticsmaterial, namely elastomers having a hardness of more than 65 Shore A,more preferably having a hardness of more than 80 Shore A. Shorehardness is defined in standards DIN 53505 and DIN 7868. One or moresieve screens or the surfaces thereof may be made of such an elastomer.

It is likewise possible to silicon-coat plastics material side-coveringsof conveying sectors for silicon chunks, for example in shaker tables.This applies equally for sampling points including plant parts in thevicinity thereof (table, suction hoods) and sampling vessels.

Likewise preferred is the passivation of elastic polyurethane facingmaterials by coating with silicon. Adhesion of the sprayed-on siliconcoat is assured even when the component parts are subjected to severemechanical deformation (bending, stretching).

The description hereinabove of illustrative embodiments is to beunderstood as being exemplary. The disclosure made thereby enables aperson skilled in the art to understand the present invention and theadvantages associated therewith and also encompasses alterations andmodifications to the described structures and processes obvious to aperson skilled in the art. All such alterations and modifications andalso equivalents shall therefore be covered by the scope of protectionof the claims.

1.-16. (canceled)
 17. A process for silicon-coating a plasticsmaterial-comprising surface of a substrate by cold gas spraying,comprising injecting a powder comprising silicon into a gas and applyingsaid powder with a high velocity to the substrate surface comprising theplastics material, such that the silicon forms a coat firmly adherent onthe substrate surface comprising the plastics material.
 18. The processof claim 17, comprising injecting the powder into nitrogen or helium ormixtures thereof
 19. The process of claim 17, wherein the powdercomprises polycrystalline silicon having grain sizes of from 20 to 80μm.
 20. The process of claim 17, wherein the silicon coat has a coatthickness between 5 and 20 μm.
 21. The process of claim 17, wherein thesurface comprising the plastics material comprises polyethylene,polypropylene, polyamide, polyurethane, polyvinylidene fluoride,polytetrafluoroethylene or ethylene tetrafluoroethylene.
 22. The processof claim 17, wherein the surface comprising the plastics materialcomprises polyurethane having a hardness of 55-95 Shore A.
 23. Theprocess of claim 17, wherein the substrate is a metallic body having asurface, and having a plastics material coating or facing on at leastpart of the surface.
 24. An apparatus which at least in part comprises asurface made of a plastics material, wherein the plastics materialsurface has a firmly adherent silicon coat prepared by the process ofclaim
 17. 25. The apparatus of claim 24 comprising a base body, aplastics material coating or a plastics material facing on at least apart of a surface of the base body and having a silicon coating on thepart of the surface of the base body coated or faced with plasticsmaterial.
 26. The apparatus of claim 25, wherein the base body of theapparatus is metallic.
 27. The apparatus of claim 25, wherein theplastics material coating or the plastics material facing comprises aforeign substance readily detectable on polycrystalline silicon.
 28. Theapparatus of claim 24, wherein the apparatus is a container made ofplastics material and having a silicon coating on its interior surface.29. The apparatus of claim 24, wherein the apparatus is a pipe made ofplastics material and having a silicon coating on its interior surface.30. The apparatus of claim 26, wherein the apparatus is a metallic pipehaving a plastics material coating or facing on its interior surface andhaving a silicon coating on the plastics material-coated or -facedinterior surface.
 31. The apparatus of claim 30, wherein the apparatusis a seed crystal feed or a product withdrawal sector in a fluidized bedreactor for producing granular polycrystalline silicon.
 32. In theproduction, further processing and logistics (packaging/transport) ofpolycrystalline silicon, where polycrystalline silicon contacts one ormore surfaces, the improvement comprising coating at least one surfacewith a silicon coating prepared by the process of claim 17.